A protein product, such as a beverage or the like, includes a mixture of water, a paste comprising protein, pH buffers, and a stabilizer. In particular, the protein product includes from about 40.00 wt. % to about 98.00 wt. % water, from about 0.50 wt. % to about 35.00 wt. % protein paste, from about 0.10 wt. % to about 0.50 wt. % sodium bicarbonate, from about 0.30 wt. % to about 0.80 wt. % calcium carbonate, and from about 0.10 wt. % to about 0.80 wt. % stabilizer. The pH of the protein product is from about 7.60 to about 8.40. The protein paste may be derived from peanuts processed at a heat load of greater than 3 and less than or equal to 2000.

A method of processing a fava bean composition is disclosed, the method comprising the steps of: i. providing a fava bean composition comprising fava beans, and ii. subjecting the fava bean composition to a betaglucosidase and at least one lactobacillus plantarum bacteria under dosage, time and temperature conditions selected so as to be sufficient to reduce the content of at least one of the compounds vicine and convicine, and preferably also at least one of the compounds divicine and isouramil, by at least 90 wt % as compared to the content of said compounds in the fava bean composition provided in step i. A fava bean composition obtained by the method as well as methods of producing food compositions using the fava bean composition and food compositions thus produced are also disclosed.

A dispersibility of a vegetable milk under a high temperature condition is increased by treating the vegetable milk with a protein deamidase. When the protein deamindase-treated vegetable milk is added to a liquid beverage or a liquid food at a high temperature, an aggregation in the protein deamindase-treated vegetable milk is prevented.

Heat treated pulse flour, pulse protein isolates obtained from heat treated pulse flour, food compositions containing such isolates, and methods for preparing heat treated pulse flours and pulse protein isolates are disclosed. The amount of volatile small molecule compounds present in the heat treated pulse flour are decreased or increased.

Treating fresh legumes includes combining fresh legumes with water to yield a mixture, heating the mixture from an initial temperature to a cooking temperature to yield a pre-cooked mixture, and heating the pre-cooked mixture at the cooking temperature to yield a cooked mixture. The cooked mixture is cooled to yield a cooled mixture, and water is removed from the cooled mixture to yield cooked legumes having an average moisture content in a range of 50 wt % to 65 wt %. A legume dough, prepared from the cooked legumes, can be sheeted and formed into legume dough pieces. The legume dough pieces may be cooked to yield a cooked legume dough product. In one example, the cooked legume dough product is a snack chip.

Disclosed are methods of processing raw leguminous materials, such as pea flour, pea concentrate, or pea isolate, to reduce non-volatile flavor components and in particular bound saponin compounds. The methods includes select processing steps by steam cooking a raw slurry to form a cooked slurry and drying the cooked slurry to form a processed material. An amount of non-volatile flavor components in the processed material is less than an amount of non-volatile flavor components in the raw materials.

A dry fractionation method and system provides for generating a protein concentrate product therefrom. The method and system includes milling a plant-based flour to generate milled flour and generating a first protein concentrate from the milled flour using an air classifier. The method and system includes processing the first protein concentrate to generate a protein rich curd and generating a neutral hydrolyzed protein slurry by mixing the protein curd with a base, water and enzymatic cocktail. The method and system includes generating a homogenized protein slurry from the protein slurry and generating a cooled protein slurry by pasteurizing the homogenized protein slurry. Therein, the method and system provides for extracting the protein concentrate product from the cooled protein slurry.

A desolventizer for processing solvent-wet solid material may include a thermal recirculation loop to increase thermal performance. In some examples, the desolventizer includes a housing, an ejector, and a vent. The housing contains a first tray and a second tray vertically elevated above the first tray to define a processing space. The ejector has an inlet located between the first tray and the second tray and an outlet also located between the first tray and the second tray. The vent has an inlet located between the first tray and the second tray. In operation, the ejector can draw gas from the processing space via the inlet and discharge the gas through the outlet back into the processing space, creating a recirculation loop.

The invention relates to a process comprising (a) providing a quantity of plant material; (b) heating the material of (a) in aqueous medium to a temperature of 75 to 105 C.; (c) physically disrupting the material of (b); (d) processing the physically disrupted material of (c) to enrich for cells and/or cell clusters; and (e) drying the material of (d). The invention also relates to a product, which comprises at least 30% or more intact plant cells, which comprises 15% or less water by weight, which has a particle size in the range 75-500 m, characterised in that the product comprises at least 30% resistant starch as a proportion of total starch. The invention also relates to foodstuffs.

In one embodiment, a method comprises adding a plurality of soybeans to an extractor, the soybeans having an average protein:oil ratio of greater than 2.3, heating the soybeans, removing hulls from the plurality of soybeans, and grinding the plurality of soybeans with water at a temperature between 180 F. and 190 F. to yield a soy extract having hexanal levels of less than 50 parts per billion (ppb).